Three-dimensionally ordered macro-porous Pt/TiO2 catalyst used for water-gas shift reaction

Three-dimensionally ordered macro-porous （3DOM） Pt/TiO2 catalysts were prepared by template and impregnation methods, and the resultant samples were characterized by using TG-DTA, XRD, SEM, TEM, and TPR techniques. The catalytic performance for water-gas shift （WGS） reaction was tested, and the influences of some conditions, such as reduction temperature of catalysts, the amount of Pt loadings and space velocity on catalytic performance were investigated. It was shown that Pt particles were homogeneously dispersed on 3DOM TiO2. The reduction of TiO2 surface was important for the catalytic performance. The activity test results showed that the 3DOM Pt/TiO2 catalysts exhibited very good catalytic performance for WGS reaction even at high space velocity, which was owing to the better mass transfer of 3DOM porous structure besides the high intrinsic activity of Pt/TiO2.     

Influence of Reaction Conditions on Methanol Synthesis and WGS Reaction in the Syngas-to-DME Process

A series of CuO-ZnO catalysts (with different Cu/Zn molar ratios) were prepared, and evaluated under the reaction conditions of syngas-to-dimethyl ether (DME) with three sorts of feed gas and different space velocity. The catalysts were characterized by X-ray diffraction (XRD) and temperature-programmed reduction (TPR). The experiment results showed that the reaction conditions of syngas-to-DME process greatly affected the methanol synthesis and WGS reaction. The influence caused by Cu/Zn molar ratio was quite different on the two reactions; increasing of percentage of CO2 in feed gas was unfavorable for catalyst activity, and also inhibited both reactions: enhancement of reaction space velocity heavily influenced the performance of the catalyst, and the benefits were relatively less for methanol synthesis than for the WGS reaction.     

Effects of reduction temperature and metal-support interactions on the catalytic activity of Pt/gamma-Al2O3 and Pt/TiO2 for the oxidation of CO in the presence and absence of H2

TiO2- and gamma-Al2O3-supported Pt catalysts were characterized by HRTEM, XPS, EXAFS, and in situ FTIR spectroscopy after activation at various conditions, and their catalytic properties were examined for the oxidation of CO in the absence and presence of H2 (PROX). When gamma-Al2O3 was used as the support, the catalytic, electronic, and structural properties of the Pt particles formed were not affected substantially by the pretreatment conditions. In contrast, the surface properties and catalytic activity of Pt/TiO2 were strongly influenced by the pretreatment conditions. In this case, an increase in the reduction temperature led to higher electron density on Pt, altering its chemisorptive properties, weakening the Pt-CO bonds, and increasing its activity for the oxidation of CO. The in situ FTIR data suggest that both the terminal and bridging CO species adsorbed on fully reduced Pt are active for this reaction. The high activity of Pt/TiO2 for the oxidation of CO can also be attributed to the ability of TiO2 to provide or stabilize highly reactive oxygen species at the metal-support interface. However, such species appear to be more reactive toward H2 than CO. Consequently, Pt/TiO2 shows substantially lower selectivities toward CO oxidation under PROX conditions than Pt/gamma-Al2O3.     

In situ characterization of Pt catalysts supported on ceria modified TiO2 for the WGS reaction: influence of ceria loading

This work analyzes the influence of cerium content (6-15 wt%) on a TiO(2) support over the structure and water gas shift (WGS) activity of Pt catalysts. The structural properties of these Pt/Ce-TiO(2) catalysts were characterized by XRD, TEM and XANES. Physicochemical characterization of the catalysts showed differences in the structure and dispersion of Ce entities on the support with Ce loading. For the samples with low ceria content (6 wt%), cerium is deposited on the support in the form of CeO(x) clusters in a highly dispersed state in close interaction with the Ti atoms. The formation of CeO(x) clusters at low Ce-loading on the support facilitates the dispersion of small particles of Pt and improves the reducibility of ceria component at low temperatures. The changes in platinum dispersion and support reducibility with Ce-loading on the TiO(2) support lead to significant differences in the WGS activity. Pt supported on the sample with lower Ce content (6 wt%) shows better activity than those corresponding to catalysts with higher Ce content (15 wt%). Activity measurements coupled with catalysts characterization suggest that the improvement in the reducibility of the support with lower Ce content was associated with the presence of CeO(x) clusters of high reducibility that improve the chemical activity of the oxide-metal interfaces at which the WGS reaction takes place.     

Kinetics of Photogenerated Electrons Involved in Photocatalytic Reaction of Methanol on Pt/TiO2

Time-resolved IR spectroscopy was used to detect the photocatalytic reaction of methanol for H2 production on Pt/TiO2 catalysts. There exists an optimal amount of Pt loading in the Pt/TiO2 catalysts for the reaction of the photogenerated long-lived electrons. For a given amount of Pt loading, the reaction rate of the long-lived electrons on Pt/TiO2 catalysts varies greatly with the di?erent reduction temperature of the catalysts. The possible reason is that the Pt particles occupy the surface active sites for methanol adsorption on Pt/TiO2 catalysts reduced at high temperature. This phenomenon is not observed obviously on Pt/TiO2 catalysts reduced at low temperature. The decay rate of the long-lived electrons evaluated by time-resolved IR method qualitatively correlates well with the activity of H2 production under steady-state irradiation conditions.     

铂基催化剂用于柴油烃氧化

The catalytic performance of Pt-based catalysts for the total oxidation of hydrocarbons was investigated.The activity of supported Pt catalysts(Pt/Al2O3,Pt/ZrO2,Pt/TiO2,and Pt/H-ZSM-5)depends on the metal oxide support.Pt/Al2O3 showed the highest catalytic activity when the catalysts were aged at 750°C for 50 h in air.The activity of Pt/Al2O3 was dependent on the valence state of the Pt surface.Pt/Al2O3 with the Pt surface in the metallic state was more active than with the surface in the cationic state.The surface density of acid and basic sites on the Al2O3 support controlled the valence state of the Pt surface and stability of the Pt particles in the highly dispersed state,respectively.     

Pt/Co3O4/3DOM Al2O3：甲苯燃烧的高效催化剂

与硫氧化物、氮氧化物、一氧化碳以及悬浮颗粒一样,大部分挥发性有机物(VOCs)污染大气环境.控制 VOCs排放有多种方法,其中催化氧化法是一种有效技术,关键在于获得高效催化剂.
　　近年来,负载过渡金属和贵金属催化剂因具有比单纯负载贵金属和单纯负载过渡金属氧化物更好的催化性能而备受关注.在负载贵金属催化剂中,高比表面积载体负载 Pt, Pd或 Rh催化剂得到广泛而深入的研究,尽管这些催化剂成本较高,但是其对 VOCs氧化反应显示了很高的低温催化活性.众所周知,催化活性取决于贵金属和 VOCs的种类,不同负载贵金属催化剂对特定反应会表现出不同的催化活性.负载 Pt催化剂对长链碳氢化合物和芳香族化合物氧化反应表现出更高的活性.相对于负载贵金属催化剂,负载过渡金属氧化物催化剂不仅具有良好的氧化活性,而且价格低廉.迄今已发现许多过渡金属氧化物(如 Co3O4, Cr2O3和 MnO2等)对典型 VOCs氧化反应具有催化活性,其中 Co3O4的催化活性尤为突出.研究表明, Co3O4的性质和分散度是决定其性能的关键因素,制备方法、载体性质和过渡金属氧化物负载量对 Co3O4的物化性质具有重要影响,而且在负载 Pt催化剂中添加金属氧化物能改善其催化性能.尽管多孔氧化铝是一种常用的载体材料,但目前尚无文献报道三维有序大孔-介孔氧化铝负载 Co3O4和 Pt纳米粒子催化剂的制备及其对甲苯氧化反应的催化性能.
　　本文采用聚甲基丙烯酸甲酯微球胶晶模板法、等体积浸渍法和聚乙烯醇保护的硼氢化钠还原法制备了三维有序大孔-介孔(3DOM Al2O3)负载 Co3O4和 Pt (xPt/yCo3O4/3DOM Al2O3, Pt的质量分数(x%)为0-1.4%, Co3O4的质量分数(y%)为0-9.2%)纳米催化剂.通过电感耦合等离子体原子发射光谱、X射线衍射、氮气吸附-脱附、扫描电子显微镜、透射电子显微镜、选区电子衍射、X射线光电子能谱及氢气程序升温还原等技术表征了催化剂的物化性质,利用固定床微型石英反应器评价了催化剂对甲苯氧化反应的催化活性.结果表明,xPt/yCo3O4/3DOMAl2O3催化剂具有多级孔结构(大孔孔径为180–200 nm,介孔孔径为4–6 nm),比表面积为94?102 m2/g.粒径为18.3 nm的 Co3O4纳米粒子和粒径为2.3?2.5 nm的 Pt纳米粒子均匀分散在3DOM Al2O3表面.在xPt/yCo3O4/3DOM Al2O3催化剂中,1.3Pt/8.9Co3O4/3DOM Al2O3拥有最高的 Oads浓度、最好的低温还原性和最高的甲苯氧化反应催化活性(当空速为20000mL g–1 h–1时,甲苯转化率达90%的反应温度为160oC).基于催化剂的活性数据和结构表征,我们认为,1.3Pt/8.9Co3O4/3DOM Al2O3优异的催化性能与其高分散的 Pt纳米粒子、高的 Oads浓度、好的低温还原性、Pt和 Co3O4纳米粒子间的强相互作用以及多级孔结构相关.     

Noble metal ionic sites for catalytic hydrogen combustion: spectroscopic insights

A catalytic hydrogen combustion reaction was carried out over noble metal catalysts substituted in ZrO(2) and TiO(2) in ionic form. The catalysts were synthesized by the solution combustion technique. The compounds showed high activity and CO tolerance for the reaction. The activity of Pd and Pt ion substituted TiO(2) was comparable and was higher than Pd and Pt ion substituted ZrO(2). The mechanisms of the reaction over the two supports were proposed by making use of the X-ray photoelectron spectroscopy and FT infrared spectroscopic observations. The reaction over ZrO(2) supported catalysts was proposed to take place by the utilization of the surface hydroxyl groups while the reaction over TiO(2) supported catalysts was hypothesized to be a hybrid mechanism utilizing surface hydroxyl groups and the lattice oxygen.     

Oxygen-deficient titania as alternative support for Pt catalysts for the oxygen reduction reaction

Insufficient electrochemical stability is a major challenge for carbon materials in oxygen reduction reaction （ORR） due to carbon corrosion and insufficient metal-support interactions. In this work, titania is explored as an alternative support for Pt catalysts. Oxygen deficient titania samples including TiO2-x and TiO2_xNy were obtained by thermal treatment of anatase TiO2 under flowing H2 and NH3, respectively. Pt nanoparticles were deposited on the titania by a modified ethylene glycol method. The samples were characterized by N2-physisorption, X-ray diffraction and X-ray photoelectron spectroscopy. The ORR activity and long-term stability of supported Pt catalysts were evaluated using linear sweep voltammetry and chronoamperometry in 0.1 mol/L HC104. Pt/TiO2_x and Pt/TiO2_xNy showed higher ORR activities than Pt/TiO2 as indicated by higher onset potentials. Oxygen deficiency in TiO2-x and TiO2-xNy contributed to the high ORR activity due to enhanced charge transfer, as disclosed by electrochemical impedance spectroscopy studies. Electrochemical stability studies revealed that Pt/TiOE_x exhibited a higher stability with a lower current decay rate than commercial Pt/C, which can be attributed to the stable oxide support and strong interaction between Pt nanoparticles and the oxygen-deficient TiO2-x support.     

纳米Pt/TiO2催化剂上气相CH3OH光催化分解制氢反应的研究

利用不同还原方法制备了不同纳米粒度的Pt/tiO2光催化剂,并且用脉冲氢氧滴定法测定了TiO2表面Pt的分散度.在气相连续流动装置中利用纳米Pt/tiO2作为光催化剂,对气相甲醇的脱氢反应进行了研究.研究了添加Pt和不添加Pt的纳米TiO2,Pt负载量、铂的不同还原方法、不同TiO2纳米粒度对气相甲醇光催化分解反应的影响,并对反应气的空速、光照时间、添加水蒸汽、改变甲醇浓度等与光催化分解甲醇制氢的关系进行了研究,在最佳反应条件下,产氢速率达到5.808 mmol/(g·h).研究了反应的动力学,得到该反应为一级反应,求得了该反应的活化能为8.53 kJ/mol,并讨论了反应机理.     

NiO/LaMnO3催化剂用于乙醇水蒸气重整反应

采用柠檬酸络合-浸渍法制备了NiO/LaMnO3钙钛矿型复合氧化物催化剂并将其应用于乙醇水蒸汽重整制氢反应, 考察了NiO含量、焙烧温度对催化剂性能的影响, 采用XRD、TPR和热分析等手段对催化剂进行了表征. 结果表明, 该催化剂具有高活性、高选择性和良好的稳定性. 催化剂中的NiO含量和焙烧温度对催化性能有显著影响. 在原料气体积组成为20%(体积分数, φ) C2H5OH 和水以及80%(φ)N2, 其中水醇摩尔比为3:1, 空速为80000 mL·h-1·g-1 cat, 反应温度为400 ℃时, 15%(质量分数, w)的NiO/LaMnO3上, 乙醇转化率接近100%. 关联催化剂活性和TPR及XRD实验结果, 发现催化剂的高活性源于由催化剂前驱体中进入钙钛矿型复合氧化物晶格中的镍离子被还原所得的金属镍.     

稀土氧化物对水煤气变换催化剂Au/CeO2性能的影响

采用沉积沉淀法制备了一系列Au/CeO2-RE2O3(RE=Nd,Eu,Sm,Y)和不同Y2O3添加量的Au/CeO2-Y2O3水煤气变换(WGS)反应催化剂,通过N2吸附-脱附、X射线粉末衍射、H2程序升温还原和Raman光谱等手段对催化剂进行了表征.结果表明,Y2O3的引入能有效提高Au/CeO2体系WGS反应的活性和稳定性,其中Ce/Y摩尔比为35时催化剂活性和稳定性最高.这是由于该添加量的Y2O3能最大程度提高Au/CeO2催化剂的结构稳定性,形成较高表面氧缺陷,有效增强Au与载体间相互作用.     

V2O5-CuO/TiO2催化剂中低温选择性催化NOx还原研究

浸渍法制备了一系列V₂O₅-CuO/TiO₂催化剂,考察中低温(200~300℃)条件下,以氨为还原剂选择性催化还原NO_x的活性,并利用比表面积及微孔孔隙分析仪(BET)、X射线衍射(XRD)对催化剂进行微观表征和分析。结果表明,500℃焙烧的2V16Cu/TiO₂催化剂展示了最佳的中低温催化活性和较宽的活性温度范围,在空速6.0×10⁴ h^-1、225℃条件下,NO_x转化率达97.3%,250℃时达到100%,温度升至300℃,催化活性仍保持在100%。XRD结果表明,随着Cu负载量的增加,逐渐显现CuO的特征峰。结合活性评价数据说明,CuO是VCu/TiO₂催化剂的主要活性组分之一,是降低SCR催化反应温度的重要因素。BET结果表明,CuO的负载对钒钛催化剂的表面结构有较大影响。耐硫性实验结果表明,添加钒氧化物制备的2V16Cu/TiO₂催化剂的抗硫性能有所改善。     

Pt对Ni2P/MCM-41催化剂加氢脱硫性能的影响

以MCM-41为载体, 采用程序升温还原法制备了含有少量Pt的Ni-P/MCM-41催化剂, 并用氢气程序升温还原(H₂-TPR)、 X射线衍射(XRD)、 N₂吸附比表面积、 X射线光电子能谱(XPS)和透射电子显微镜(TEM)对催化剂的结构和性能进行了表征. 考察了P/Ni摩尔比及Pt含量对Ni-P/MCM-41催化剂催化二苯并噻吩(DBT)加氢脱硫(HDS)性能的影响. 结果表明, Pt能降低Ni₂P催化剂的还原温度, 并有助于Ni₂P相的生成, 抑制团聚现象, 提高催化剂的HDS活性. 当Pt的质量分数为0.6%, P/Ni摩尔比为2时, 催化剂具有最佳加氢脱硫活性, 在340 ℃, 3.0 MPa, 氢油体积比为500, 质量空速(WHSV)为2.0 h^-1的条件下, 二苯并噻吩转化率为100%, 且催化剂加氢脱硫活性在120 h内基本保持稳定.     

Pt/CeO2-ZrO2变换催化剂的制备、表征与性能

 用共沉淀法制备了不同Ce/Zr比的CeO2-ZrO2复合氧化物,用浸渍法制备了Pt/CeO2-ZrO2水煤气变换催化剂,并对该催化剂进行了活性评价. 结果表明,与传统的Cu基低变催化剂相比,该催化剂具有操作温度范围宽和抗氧化冲击等优点,具有应用于车载重整制氢过程的潜力. 考察了温度、空速和汽/气比等条件对催化剂活性的影响,对催化剂的制备参数和工艺参数进行了研究. 结果表明,不同Ce/Zr比的Pt/CeO2-ZrO2催化剂的活性相差很大,其中Pt/Ce0.8Zr0.2O2变换催化剂活性最高. XRD结果表明,制备的Pt/Ce0.8Zr0.2O2形成了固溶体. 通过增加单位质量催化剂表面的Pt原子数可提高催化剂的活性.     

The First Study on the Reactivity of Water Vapor in Metal–Organic Frameworks with Platinum Nanocrystals

We first studied the reactivity of H₂O vapor in metal–organic frameworks (MOFs) with Pt nanocrystals (NCs) through the water–gas shift (WGS) reaction. A water‐stable MOF, UiO‐66, serves as a highly effective support material for the WGS reaction compared with ZrO₂. The origin of the high catalytic performance was investigated using in situ IR spectroscopy. In addition, from a comparison of the catalytic activities of Pt on UiO‐66, where Pt NCs are located on the surface of UiO‐66 and Pt@UiO‐66, where Pt NCs are coated with UiO‐66, we found that the competitive effects of H₂O condensation and diffusion in the UiO‐66 play important roles in the catalytic activity of Pt NCs. A thinner UiO‐66 coating further enhanced the WGS reaction activity of Pt NCs by minimizing the negative effect of slow H₂O diffusion in UiO‐66.     

Effects of calcium ions on solubility and aggregation behavior of an anionic sulfonate gemini surfactant in aqueous solutions

In this work, a ternary composite, Pt/TiO(2)/RGO (reduced graphite oxide), was prepared via immobilizing Pt particles onto the TiO(2)/RGO composite that was obtained via redox reaction of TiCl(3) and GO. The composite was characterized by different techniques including X-ray diffraction, transmission electron microscopy, and X-ray photoelectron spectroscopy. The TiO(2) particles with size less than 10 nm were uniformly distributed throughout the RGO, and almost each Pt particle with size around 3 nm adhered to TiO(2) particles, resulting in high dispersion of all Pt particles on the support. The Pt particles were in the electron-deficient state due to the strong interactions with the TiO(2) particles and the RGO support. The catalytic performance of the composite for nitrobenzene hydrogenation was investigated under solvent-free condition. It was indicated that the Pt/TiO(2)/RGO catalyst exhibited high activity with a turnover frequency (e.g., 59,000 h(-1)) as well as superior selectivity to aniline (e.g., >99%). Moreover, the catalyst can be reused for six times without any activity loss, which resulted from the stable structure of the catalyst.     

Copper Promoted Au/ZnO-CuO Catalysts for Low Temperature Water-gas Shift Reaction

IntroductionThe water-gas shift(WGS)reaction is an impor-tant step in many important chemical processes[1].Re-cently,the renewed interest in the removal of CO bythe WGS reaction has grown significantly because of theincreasing attention to pure hydrogen p…     

负载型铈基催化剂在NH3-SCR反应中的载体效应

近年来,氨-选择催化还原(NH3-SCR)技术被公认为是控制燃煤烟气和柴油车尾气氮氧化物(NOx)排放的最有效手段之一.V2O5-WO3/TiO2和V2O5-MoO3/TiO2催化剂在300–400°C范围内表现出优异的脱硝性能和抗H2O和SO2中毒性能,因而被广泛用于NH3-SCR过程.然而,钒基催化剂存在一些缺点,如氧化SO2到SO3的活性较高、高温下将部分NH3非选择性地氧化成N2O、V2O5具有生物毒性等.因此,非钒基脱硝催化剂的研制引起人们越来越多的关注.二氧化铈(CeO2)因具有氧化还原性能优异、储/释氧能力强和Ce3+/Ce4+转换容易等优点而广泛用于NH3-SCR反应.然而,单纯CeO2的脱硝性能并不理想.研究表明,将CeO2制备成铈基复合金属氧化物催化剂和负载型铈基催化剂可显著提高其在NH3-SCR反应中的催化性能.尤其是负载型铈基催化剂由于催化性能优异、比表面积大、热稳定性高及活性组分用量少而成为研究热点.众所周知,对于负载型金属氧化物催化剂,载体并不只是惰性材料,它会显著影响表面负载组分的物理化学性质和催化性能.因此,关于载体与组分间相互作用的研究常见诸报道.但是,对于负载型铈基催化剂,具有不同晶相结构的载体对其理化性质和NH3-SCR催化性能的影响规律尚不明晰.此外,SiO2,γ-Al2O3,ZrO2和TiO2是工业上常用的四种催化剂载体,它们具有不同的晶相结构和应用场合,究竟哪一个最适合作为负载型铈基催化剂的载体用于NH3-SCR反应尚无定论.因此,为了阐明负载型铈基催化剂在NH3-SCR反应中的载体效应,筛选出最佳的催化剂载体,我们首先采用溶胶-凝胶法和沉淀法合成了SiO2,γ-Al2O3,ZrO2和TiO2四个载体,再通过浸渍法制备了一系列负载型铈基催化剂(CeO2/SiO2,CeO2/γ-Al2O3,CeO2/ZrO2和CeO2/TiO2)用于NH3-SCR反应.并借助于X射线衍射(XRD)、拉曼光谱(Raman)、比表面积测定(BET)、X射线光电子能谱(XPS)、氢气-程序升温还原(H2-TPR)以及氨气-程序升温脱附(NH3-TPD)等表征手段对上述载体和催化剂进行了较为全面的分析.研究结果表明,这些负载型铈基催化剂的理化性质和脱硝性能强烈地依赖于催化剂载体.首先,CeO2/γ-Al2O3催化剂的表面Ce3+含量明显大于CeO2/SiO2,CeO2/ZrO2和CeO2/TiO2催化剂,有利于氧空位的产生以促进NO分子的解离,进而导致优异的NH3-SCR反应性能.其次,CeO2/γ-Al2O3催化剂具有最佳的还原性能,有利于NO氧化为NO2,进而通过"快速NH3-SCR"途径提升其催化性能.再者,CeO2/γ-Al2O3催化剂表面酸性位最多,能够促进反应物NH3分子的吸附与活化,从而提高脱硝性能.最后,CeO2/γ-Al2O3催化剂在H2O和SO2存在的条件下同样表现出最佳的催化性能,表明其有望用于实际燃煤烟气脱硝.     

NiO/WO3/TiO2-Al2O3催化剂上正庚烷的临氢异构化

采用溶胶凝胶法制备了TiO2-Al2O3复合载体,用分步浸渍法制备了NiO/WO3/TiO2-Al2O3催化剂。 在常压连续流动固定床反应器上考察了NiO/WO3/TiO2-Al2O3对正庚烷临氢异构化反应的催化性能。 研究了催化剂中WO3含量、Ni含量、焙烧温度和还原温度及催化反应温度对临氢异构化反应的影响。 采用XRD和BET方法对催化剂进行了表征。 结果表明,当w(WO3)=25%、w(Ni)=10%时,所制备的NiO/WO3/TiO2-Al2O3催化剂对正庚烷异构化反应的催化性能最好,活性可达15.50%,选择性可达84.06%。